Catalyst system comprising two zirconocenes and aluminoxane

ABSTRACT

A catalyst system comprising an aluminoxane and a transition-metal component (metallocene) is used, the transition-metal component comprising at least one zirconocene of the formula I ##STR1## and at least one zirconocene of the formula Ia or alternatively at least 2 zirconocenes of the formula I.

This is a divisional of Ser. No. 08/119,893, filed Sep. 10, 1993, now U.S. Pat. No. 5,350,817, which is a continuation of Ser. No. 07/880,097 filed May 22, 1992, now abandoned.

It is known that metallocene catalysts in combination with aluminoxanes are capable of polymerizing olefins to give polyolefins having a narrow molecular weight distribution (M_(w) /M_(n) of 2-3) (J. Polym. Sci., Pol. Chem. Ed. 3 (1985) 2117; EP-A 302 424). Polyolefins of this type with a narrow distribution are suitable, for example, for applications in precision injection molding, injection molding in general and for the production of fibers. For numerous applications, such as, for example, thermoforming, extrusion, blow molding and for the production of polyolefin foams and films, broader or bimodal molecular weight distributions are required.

For polyethylene, it has been proposed to achieve such products by using two or more metallocene catalysts in the polymerization (EP-A 128 045); however, the systems described are achiral catalysts and would give atactic polypropylene on polymermization of propene. However, atactic polypropylene is unsuitable as a structural material.

The preparation of stereoblock polypropylene where M_(w) /M_(n) is 13-15 is disclosed in DE-A 3 640 924. These catalyst systems are likewise unsuitable for the formation of polyolefins of high tacticity. Furthermore, the metallocene activities which can be achieved at industrially relevant polymerization temperatures and the molecular weights of polymer products are too low. In addition, the proposed catalysts give only an atactic polymer at such polymerization temperatures.

EP-A 310 734 proposes catalyst systems comprising a mixture of a hafnocene and a zirconocene for the preparation of polypropylene. Products have broad to bimodal distributions where M_(w) /M_(n) is from 3.7 to 10.3

If only the hafnocene catalyst is used, polypropylene with a broad distribution is obtained at a certain polymerization temperature, according to EP-A 355 439.

Syndiotactic polypropylene having a broad distribution is described in EP-A 387 691 (M_(w) /M_(n) up to 6.4) if a hafnocene is used.

These processes have the common disadvantages of hafnium catalyst costs which are too high for industrial applications, together with a low polymerization activity, which additionally makes it necessary to carry out thorough, high-cost purification of the prepared polymer to remove catalyst residues.

The object was thus to find a catalyst system and a process by means of which polyolefins having a broad, bimodal or multimodal distribution can be prepared and which avoid the disadvantages known from the prior art.

The object is achieved by using a catalyst system comprising at least two stereorigid zirconocenes and an aluminum compound as cocatalyst.

The invention thus relates to a process for the preparation of a polyolefin which has a molecular weight distribution M_(w) /M_(n) of ≧3.0 and which may be monomodal, bimodal or multimodal, by polymerization or copolymerization of an olefin of the formula R^(a) CH═CHR^(b) in which R^(a) and R^(b) are identical or different and a hydrogen atom or a alkyl radical having 1 to 14 carbon atoms, or R^(a) and R^(b), together with the atoms connecting them, can form a ring, at a temperature of from -60° to 200° C., at a pressure of from 0.5 to 100 bar, in solution, in suspension or in the gas phase, in the presence of a catalyst comprising a transition-metal component (metallocene) and an aluminoxane of the formula II ##STR2## for the linear type and/or of the formula III ##STR3## for the cyclic type, where, in the formulae II and III, the radicals R may be identical or different and are a C₁ -C₆ -alkyl group, a C₁ -C₆ -fluoroalkyl group, a C₆ -C₁₈ -aryl group, a C₁ -C₆ -fluoroaryl group or a hydrogen, and n is an integer from 0 to 50, or, instead of the aluminoxane, comprises a mixture of an aluminoxane of the formula II and/or of the formula III with a compound AlR₃, which comprises using, as the transition-metal component, at least one zirconocene of the formula I and at least one zirconocene of the formula Ia or alternatively at least 2 zirconocenes of the formula I ##STR4## in which R¹ and R² are identical or different and are a hydrogen atom, a C₁ -C₁₀ -alkyl group, a C₁ -C₁₀ -alkoxy group, a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -aryloxy group, a C₂ -C₁₀ -alkenyl group, a C₇ -C₄₀ -arylalkyl group, a C₇ -C₄₀ -alkylaryl group, a C₈ -C₄₀ -arylalkenyl group or a halogen atom,

R³ and R⁴ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group, which may be halogenated, a C₆ -C₁₀ -aryl group, or a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or --PR₂ ¹⁰ radical, in which R¹⁰ is a halogen atom, a C₁ -C₁₀ -alkyl group or a C₆ -C₁₀ -aryl group,

R⁵ and R⁶ are identical or different and are as defined for R³ and R⁴, with the proviso that R⁵ and R⁶ are not hydrogen,

R⁷ is ##STR5## ═BR¹¹, ═AlR¹¹, --Ge--, --Sn, --O--, --S--, ═SO, ═SO₂, ═NR¹¹, ═CO, ═PR¹¹ or ═P(O)R¹¹,

where

R¹¹, R¹² and R¹³ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group, a C₁ -C₁₀ -fluoroalkyl group, a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -fluoroaryl group, a C₁ -C₁₀ -alkoxy group, a C₂ -C₁₀ -alkenyl group, a C₇ -C₄₀ -arylalkyl group, a C₈ -C₄₀ -arylalkenyl group or a C₇ -C₄₀ -alkylaryl group, or R¹¹ and R¹² or R¹¹ and R¹³, together with the atoms connecting them, in each case form a ring, and

M¹ is silicon, germanium or tin,

R⁸ and R⁹ are identical or different and are as defined for R¹¹,

R¹⁴ and R¹⁵ are identical or different and are a monocyclic or polycyclic hydrocarbon radical which can form a sandwich structure together with the zirconium atom, and

m and n are identical or different and are zero, 1 or 2, where m plus n is zero, 1 or 2.

Alkyl is straight-chain or branched alkyl. Halogen (halogenated) refers to fluorine, chlorine, bromine or iodine, preferably fluorine or chlorine.

R¹ and R² are identical or different and are a hydrogen atom, a C₁ -C₁₀ -, preferably C₁ -C₃ -alkyl group, a C₁ -C₁₀ -, preferably C₁ -C₃ -alkoxy group, a C₆ -C₁₀ -, preferably C₆ -C₈ -aryl group, a C₆ -C₁₀ -, preferably C₆ -C₈ -aryloxy group, a C₂ -C₁₀ -, preferably C₂ -C₄ -alkenyl group, a C₇ -C₄₀ -, preferably C₇ -C₁₀ -arylalkyl group, a C₇ -C₄₀ -, preferably C₇ -C₁₂ -alkylaryl group, a C₈ -C₄₀ -, preferably C₈ -C₁₂ -arylalkenyl group, or a halogen atom, preferably chlorine.

R³ and R⁴ are identical or different and are a hydrogen atom, a halogen atom, preferably fluorine, chlorine or bromine atom, a C₁ -C₁₀ -, preferably C₁ -C₄ -alkyl group, which may be halogenated, a C₆ -C₁₀ -, preferably C₆ -C₈ -aryl group, a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or --PR₂ ¹⁰ radical in which R¹⁰ is a halogen atom preferably a chlorine atom, or a C₁ -C₁₀ -, preferably C₁ -C₃ -alkyl group or a C₆ -C₁₀ -, preferably C₆ -C₈ -aryl group. R³ and R⁴ are particularly preferably hydrogen.

R⁵ and R⁶ are identical or different, preferably identical, and are as defined for R³ and R⁴, with the proviso that R⁵ and R⁶ cannot be hydrogen. R⁵ and R⁶ are preferably (C₁ -C₄)-alkyl, which may be halogenated, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl or trifluoromethyl, in particular methyl.

R⁷ is ##STR6## ═BR¹¹, ═AlR¹¹, --Ge--, --Sn, --O--, --S--, ═SO, ═SO₂, ═NR¹¹, ═CO, ═PR¹¹ or ═P(O)R¹¹, where R¹¹, R¹² and R¹³ are identical or different and are hydrogen atoms, halogen atoms, a C₁ -C₁₀ -, preferably C₁ -C₄ -alkyl group, in particular methyl group, a C₁ -C₁₀ -fluoroalkyl group, preferably CF₃ group, a C₆ -C₁₀ -, preferably C₆ -C₈ -aryl group, a C₆ -C₁₀ -fluoroaryl group, preferably pentafluorophenyl group, a C₁ -C₁₀ -, preferably C₁ -C₄ -alkoxy group, in particular methoxy group, a C₂ -C₁₀ -, preferably C₂ -C₄ -alkenyl group, C₇ -C₄₀ -, preferably C₇ -C₁₀ -arylalkyl group, a C₈ -C₄₀ -, preferably C₈ -C₁₂ -arylalkenyl group, or a C₇ -C₄₀ -, preferably C₇ -C₁₂ -alkylaryl group, or R¹¹ and R¹² or R¹¹ and R¹³, together with the atoms connecting them, in each case form a ring.

M¹ is silicon, germanium or tin, preferably silicon or germanium.

R⁷ is preferably ═CR¹¹ ═R¹², ═SiR¹¹ R¹², ═GeR¹¹ R¹², --O--, --S--, ═SO, ═PR¹¹ or ═P(O)R¹¹.

R⁸ and R⁹ are identical or different and are as defined for R¹¹.

m and n are identical or different and are zero, 1 or 2, preferably zero or 1, where m plus n is zero, 1 or 2, preferably zero or 1.

R¹⁴ and R¹⁵ are preferably fluorenyl, indenyl or cyclopentadienyl, it being possible for these parent structures also to carry additional substituents as defined for R¹¹.

Particularly preferred metallocenes are thus those in which, in the formula I, R¹ and R² are identical or different and are methyl or chlorine, R³ and R⁴ are hydrogen, R⁵ and R⁶ are identical or different and are methyl, ethyl or trifluoromethyl, R⁷ is a ##STR7## radical, and n plus m is zero or 1, in particular the compounds listed in the working examples.

Of the compounds I mentioned in the working examples, rac-dimethylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride, rac-ethylene(2-methyl-1-indenyl)₂ zirconium dichloride, rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride, rac-methylethylene(2-methyl-1-indenyl)₂ zirconium dichloride and rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride are of particular importance.

The particularly preferred metallocenes of the formula Ia are those in which R¹ and R² are identical or different and are methyl or chlorine,

R⁷ is a ##STR8## radical, n+m is zero or 1 and

R¹⁴ and R¹⁵ are identical or different and are fluorenyl, indenyl or substituted cyclopentadienyl, in particular the compounds Ia listed in the working examples.

Of particular importance are thus rac-phenyl(methyl)silyl(indenyl)₂ zirconium dichloride, diphenylmethylene(9-fluorenyl)(cyclopentadienyl)zirconium dichloride, isopropylidene(9-fluorenyl)(cyclopentadienyl)zirconium dichloride, rac-dimethylsilyl(2,3,5-trimethyl-1-cyclopentadienyl)₂ zirconium dichloride, rac-dimethylsilyl(indenyl)₂ zirconium dichloride, rac-dimethylgermyl(indenyl)₂ zirconium dichloride, rac-dimethylsilyl(indenyl)₂ dimethylzirconium, rac-phenyl(vinyl)silyl(indenyl)₂ zirconium dichloride, ##STR9## rac-dimethylsilyl(2,4-dimethylcyclopentadienyl)₂ zirconium dichloride, rac-isopropylidene(indenyl)₂ zirconium dichloride, rac-dimethylsilyl(2-methyl-4,5,6,7-tetrahydro-1-indenyl)₂ zirconium dichloride, rac-ethylene(indenyl)₂ zirconium dichloride, rac-methylene(3-t-butyl-1-cyclopentadienyl)₂ zirconium dichloride and rac-dimethylsilyl(4,7-dimethyl-1-indenyl)₂ zirconium dichloride.

The metallocenes having C₅ symmetry (subgroup of compounds of the formula Ia; for example R¹¹ R¹² C(fluorenyl)(cyclopentadienyl)dimethylzirconium) are employed for the preparation of the syndiotactic block in the polyolefin.

For the purposes of the present invention, the term C₅ symmetry means that the corresponding metallocenes have a mirror plane perpendicular to the plane passing through Zr, R¹ and R². The bisecting line of the angle R¹ --Zr--R² extends in this mirror plane. This consideration of symmetry is restricted to part of the zirconocene molecule, i.e. the --(CR⁸ R⁹)_(n) --R⁷ --(CR⁸ R⁹)_(m) -- bridge is not taken into account. Furthermore, the term C₅ symmetry should be understood in formal or idealized terms. Thus, for example, shifts in said moiety which may be caused by the bridge and can only be explained via the structure are not considered for the purposes of the present invention.

The chiral metallocenes are employed as racemates for the preparation of highly isotactic polyolefins. However, it is also possible to use the pure R- or S-form. These pure stereoisomeric forms allow preparation of an optically active polymer. However, the meso-form of the metallocenes should be removed since the polymerization-active center (the metal atom) in these compounds is no longer chiral due to mirror symmetry at the central metal and can therefore not produce any highly isotactic polymer. If the meso-form is not removed, atactic polymer is formed alongside isotactic polymer. For certain applications--soft moldings for example--this may be thoroughly desirable.

The principle of resolution of stereoisomers is known.

The metallocenes I and Ia can be prepared by the principle of the following reaction scheme: ##STR10## (cf. Journal of Organomet. Chem. (1985) 63-67 and EP-A 320762).

The choice of the metallocenes for the polymerization of olefins to give polyolefins having a broad or multimodal distribution can take place by means of a test polymerization for each metallocene.

In this test, the olefin is polymerized to the polyolefin and the mean molecular weight M_(w) thereof and the molecular weight distribution M_(w) /M_(n) thereof are determined by means of gel permeation chromatography. Depending on the desired molecular weight distribution, the metallocenes are then combined.

Taking into account the polymerization activities, it is then possible, by means of computer simulation of the combined gel permeation curves, to directly produce any desired molecular weight distribution via the type of metallocenes and via the ratio of the amounts of the metallocenes to one another.

The number of zirconocenes to be used according to the invention is preferably 2 or 3, in particular 2. However, it is also possible to use a greater number (such as, for example, 4 or 5) in any desired combination of I and Ia.

By including the polymerization activities and molecular weights at various polymerization temperatures, in the presence of hydrogen as molecular weight regulator or in the presence of comonomers, the computer simulation model can be further refined and the applicability of the process according to the invention further improved.

The cocatalyst used is an aluminoxane of the formula II and/or III, where n is an integer from 0 to 50, preferably 10 to 35.

The radicals R are preferably identical and are methyl, isobutyl, phenyl or benzyl, particularly preferably methyl.

If the radicals R are different, they are preferably methyl and hydrogen or alternatively methyl and isobutyl, hydrogen or isobutyl preferably being present to the extent of 0.01-40% (number of radicals R). The aluminoxane can be replaced as cocatalyst in the polymerization by a mixture comprising aluminoxane and AlR₃, where R is as defined above.

The aluminoxane can be prepared in various ways by known processes. One of the methods is, for example, to react an aluminum hydrocarbon compound and/or a hydridoaluminum hydrocarbon compound with water (gaseous, solid, liquid or bound--for example as water of crystallization) in an inert solvent (such as, for example, toluene). To prepare an aluminoxane containing different alkyl groups R, two different trialkylaluminum compounds (AlR₃ +AlR'₃), corresponding to the desired composition, are reacted with water (cf. S. Pasynkiewicz, Polyhedron 9 (1990) 429 and EP-A 302 424).

The precise structure of the aluminoxanes II and III is unknown.

Irrespective of the preparation method, all aluminoxane solutions have in common a varying content of unreacted aluminum starting compound, which is in free form or as an adduct.

It is possible, before use in the polymerization reaction, to preactivate the metallocenes, in each case separately or together as a mixture, by means of an aluminoxane of the formula (II) and/or (III). This significantly increases the polymerization activity and improves the particle morphology.

The preactivation of the metallocenes is carried out in solution. The metallocenes are preferably dissolved, as solids, in a solution of the aluminoxane in an inert hydrocarbon. Suitable inert hydrocarbons are aliphatic or aromatic hydrocarbons. Toluene or a C₆ -C₁₀ -hydrocarbon is preferably used.

The concentration of the aluminoxane in the solution is in the range from about 1% by weight to the saturation limit, preferably from 5 to 30% by weight, in each case based on the total solution. The metallocenes can be employed in the same concentration, but are preferably employed in an amount of from 10⁻⁴ -1 mole per mole of aluminoxane. The preactivation time is from 5 minutes to 60 hours, preferably from 5 to 60 minutes. The temperature used is from -78° C. to 100° C., preferably from 0° to 70° C.

The metallocenes may also be prepolymerized or applied to a support. Prepolymerization is preferably carried out using the (or one of the) olefin(s) employed in the polymerization.

Examples of suitable supports are silica gels, aluminum oxides, solid aluminoxane or other inorganic support materials. Another suitable support material is a polyolefin powder in finely divided form.

A further possible embodiment of the process according to the invention comprises using a salt-like compound of the formula R_(x) NH_(4-x) BR'₄ or of the formula R₃ PHBR'₄ as cocatalyst in place of or in addition to an aluminoxane. In these formulae, x=1, 2 or 3, R=alkyl or aryl, identical or different, and R'=aryl, which may also be fluorinated or partially fluorinated. In this case, the catalyst comprises the product of the reaction of the metallocenes with one of said compounds (cf. EP-A 277 004).

In order to remove the catalyst poisons present in the olefin, purification by means of an alkylaluminum compound, for example AlMe₃ or AlEt₃, is advantageous. This purification can be carried out either in the polymerization system itself, or the olefin is brought into contact with the Al compound before addition to the polymerization system and is subsequently removed again.

The polymerization or copolymerization is carried out in a known manner in solution, in suspension or in the gas phase, continuously or batchwise, in one or more steps, at a temperature of from -60° to 200° C., preferably from 20° to 80° C. Olefins of the formula R^(a) --CH═CH--R^(b) are polymerized or copolymerized. In this formula R^(a) and R^(b) are identical or different and are hydrogen atoms or alkyl radicals having 1 to 14 carbon atoms. However, R^(a) and R^(b) may also form a ring with the carbon atoms connecting them. Examples of such olefins are ethylene, propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene, norbornene and norbornadiene. In particular, propylene and ethylene are polymerized.

If necessary, hydrogen is added as molecular weight regulator. The various hydrogen-reactivities of the metallocenes and the possibility of changing the amount of hydrogen during the polymerization can result in a further desired broadening of the molecular weight distribution.

The overall pressure in the polymerization system is from 0.5 to 100 bar. The polymerization is preferably carried out in the industrially particularly interesting pressure range of from 5 to 64 bar.

The metallocenes are used in a concentration, based on the transition metal, of from 10⁻³ to 10⁻⁸ mol, preferably from 10⁻⁴ to 10⁻⁷ mol, of transition metal per dm³ of solvent or per dm³ of reactor volume. The aluminoxane or the aluminoxane/AlR₃ mixture is used in a concentration of from 10⁻⁵ to 10⁻¹ mol, preferably from 10⁻⁴ to 10⁻² mol, per dm³ of solvent or per dm³ of reactor volume. In principle, however, higher concentrations are also possible.

If the polymerization is carried out as a suspension or solution polymerization, an inert solvent which is customary for the Ziegler low-pressure process is used. For example, the polymerization is carried out in an aliphatic or cycloaliphatic hydrocarbon; the examples of these which may be mentioned are butane, pentane, hexane, heptane, decane, isooctane, cyclohexane and methylcyclohexane. It is also possible to use a gasoline or hydrogenated diesel oil fraction. Toluene can also be used. The polymerization is preferably carried out in the liquid monomer.

If inert solvents are used, the monomers are metered in in gaseous or liquid form.

The polymerization can take as long as desired, since the catalyst system used according to the invention only exhibits a slight decrease in the polymerization activity with time.

The process according to the invention is distinguished by the fact that the metallocenes described give polymers having a broad, bimodal or multimodal molecular weight distribution, high molecular weight, high stereospecificity and good particle morphology in the industrially interesting temperature range between 20° and 80° C. with high polymerization activity.

The polymers according to the invention are particularly suitable for the production of films, in particular transparent films, thermoforming applications, polyolefin foams, extrusion applications and for the production of transparent hollow articles and for blow molding in general.

The examples below are intended to illustrate the invention in greater detail.

The following abbreviations are used:

VN=viscosity number in cm³ /g ##EQU1## MFI (230/5)=melt flow index, measured in accordance with DIN 53735; melt temperature 230° C. and weight 5 kg.

EXAMPLE 1

A dry24 dm³ reactor was flushed with nitrogen and filled with 12 dm³ of liquid propylene. 39 cm³ of a toluene solution of methylaluminoxane (corresponding to 52 mmol of Al, mean degree of oligomerization of the methylaluminoxane was n=19) were then added, and the batch was stirred at 30° C. for 15 minutes.

In parallel, 13.5 mg (0.025mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 51.0 mg (0.10 mmol) of rac-phenyl(methyl)silyl(1-indenyl)zirconium dichloride were dissolved in 15 cm³ of a toluene solution of methylaluminoxane (20 mmol), and the solution was introduced into the reactor after 15 minutes.

The mixture was polymerized at 30° C. for 3 hours. The polymerization was terminated by addition of 12 l of CO₂ gas. 1.85 kg of polypropylene were obtained, corresponding to an activity of the metallocene mixture of 9.6 kg of PP/g of metallocene×h.

VN=331 cm³ /g; M_(w) =411,000 g/mol, M_(w) /M_(n) =8.5; II=96.9%.

EXAMPLE 2

Example 1 was repeated, but the metallocene mixture components employed were 11.2 mg (0.025 mmol) of rac-ethylene(2-methyl-1-indenyl)₂ zirconium chloride and 13.9 mg (0.025 mmol) of diphenylmethylene(9-fluorenyl)(cyclopentadienyl)zirconium dichloride; the polymerization temperature was 60° C. and the polymerization time was 1 hour.

2.45 kg of polypropylene were obtained, corresponding to an activity of the metallocene mixture of 97.6 kg of PP/g of metallocene×h.

VN=255 cm³ /g; M_(w) =385,000 g/mol, M_(w) /M_(n) =7.5.

The resultant polymer could be separated by fractionation into a fraction of isotactic polypropylene (II>96%) and a fraction of syndiotactic polypropylene (SI>96%). The mixing ratio was about 1:1.

EXAMPLE 3

Example 1 was repeated, but the metallocene mixture components employed were 5.4 mg (0.010 mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 5.4 mg (0.013 mmol) of dimethylmethylene(9-fluorenyl)(cyclopentadienyl)zirconium dichloride, the polymerization temperature was 70° C. and the polymerization time was 1 hour.

2.2 kg of a mixture of about two parts of isotactic polypropylene and one part of syndiotactic polypropylene were obtained, corresponding to an activity of the metallocene mixture of 203.7 kg of PP/g of metallocene×h.

VN=172 cm³ /g; M_(w) =186,500 g/mol, M_(w) /M_(n) =3.0.

EXAMPLE 4

Example 1 was repeated, but the metallocene mixture components employed were 4.8 mg (0.01 mmol) of rac-Me₂ Si(2-methyl-1-indenyl)₂ zirconium dichloride and 21.2 mg (0.05 mmol) of rac-Me₂ Si(2,3,5-trimethylcyclopentadienyl)₂ zirconium dichloride, and the polymerization temperature was 50° C.

2.57 kg of polypropylene were obtained, corresponding to an activity of the metallocene mixture of 32.9 kg of PP/g of metallocene×h.

VN=194 cm³ /g; M_(w) =261,000 g/mol, M_(w) /M_(n) =7.9, II=98.5%.

EXAMPLE 5

Example 1 was repeated, but the metallocene mixture components employed were 4.5 mg (0.008 mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 6.6 mg (0.015 mmol) of rac-dimethylsilyl(indenyl)₂ zirconium dichloride. The polymerization time was one hour, and the polymerization temperature was 50° C.

1.35 kg of polypropylene were obtained, corresponding to an activity of the metallocene mixture of 121.6 kg of PP/g of metallocene×h.

VN=154 cm³ /g; M_(w) =133,000 g/mol, M_(w) /M_(n) =5.2, II=96.0%.

EXAMPLE 6

Example 1 was repeated, but the metallocene mixture components employed were 2.4 mg (0.005 mmol) of rac-dimethylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 2.5 mg (0.005 mmol) of rac-dimethylgermyl(indenyl)₂ zirconium dichloride. The two metallocenes were dissolved separately, each in 7.5 cm³ of a toluene solution of methylaluminumoxane, and after 15 minutes these solutions were metered into the polymerization system. The mixture was polymerized at 70° C. for 1 hour.

1.57 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 320.4 kg of PP/g of metallocene×h.

VN=105 cm³ /g; M_(w) =114,000 g/mol, M_(w) /M_(n) =4.1, II=96.3%.

EXAMPLE 7

Example 6 was repeated, but the metallocenes used were 4.8 mg (0.01 mmol) of rac-dimethylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 1.5 mg (0.004 mmol) of rac-dimethylsilyl(indenyl)_(w) dimethylzirconium.

2.08 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 330.2 kg of PP/g of metallocene×h.

VN=121 cm³ /g; M_(w) =101,900 g/mol, M_(w) /M_(n) =4.0, II=96.0%.

EXAMPLE 8

Example 6 was repeated, but the metallocenes used were 2.7 mg (0.005 mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 20.5 mg (0.04 mmol) of rac-phenyl(vinyl)silyl(indenyl)₂ zirconium dichloride.

2.17 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 93.5 kg of PP/g of metallocene×h.

VN=102 cm³ /g; M_(w) =79,400 g/mol, M_(w) /M_(n) =3.3, II=96.9%.

EXAMPLE 9

Example 6 was repeated, but the metallocenes used were 4.8 mg (0.01 mmol) of rac-dimethylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 9.2 mg (9.02 mmol) of ##STR11##

1.82 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 130 kg of PP/g of metallocene.

VN=145 cm³ /g; M_(w) =185,500 g/mol, M_(w) /M_(n) =3.6, II=96.8%.

EXAMPLE 10

Example 6 was repeated, but the metallocenes used were 2.7 mg (0.005mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 2.4 mg (0.006 mmol) of rac-dimethylsilyl(2,4-dimethylcyclopentadienyl)₂ zirconium dichloride.

1.31 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 256.9 kg of PP/g of metallocene×h.

VN=118 cm³ /g; M_(w) =129,500 g/mol, M_(w) /M_(n) =3.8, II=98.0%.

EXAMPLE 11

Example 1 was repeated, but the metallocenes used were 26.9 mg (0.05mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 32.5 mg (0.08 mmol) of rac-dimethylsilyl(2,4-dimethylcyclopentadienyl)₂ zirconium dichloride. The polymerization time was 2 hours. 2.32 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 19.5 kg of PP/g of metallocene×h.

VN=386 cm³ /g; M_(w) =436,000 g/mol, M_(w) /M_(n) =7.2, II=98.5%.

EXAMPLE 12

Example 1 was repeated, but the metallocenes used were 9.2 mg (0.02 mmol) of rac-methylethylene(2-methyl-1-indenyl)₂ zirconium dichloride and 8.6 mg (0.02 mmol) of rac-dimethylmethylene(1-indenyl)₂ zirconium dichloride, and the polymerization temperature was 50° C. 1.42 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 26.6 kg of PP/g of metallocene×h.

VN=101 cm³ /g; M_(w) =123,000 g/mol, M_(w) /M_(n) =8.5, II=91.6%.

EXAMPLE 13

A dry 24 dm³ reactor was flushed with nitrogen and filled with 24 dm³ (s.t.p.) of hydrogen and 12 dm³ of liquid propylene.

10 ml of a toluene solution of trimethylaluminum (corresponding to 26 mol of AlMe₃) were then added, and the batch was stirred at 40° C. for 15 minutes.

In parallel, 5.4 mg (0.01 mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 4.9 mg (0.01 mmol) of rac-dimethylgermyl(indenyl)₂ zirconium dichloride were dissolved in 15 cm³ of methylaluminoxane solution (20 mmol of Al, toluene), and, after 15 minutes, the solution was introduced into the reactor. The reactor contents were heated to 65° C. in 3 minutes and polymerized at this temperature for one hour.

The polymerization was terminated by addition of 12 l of CO₂ gas, excess propylene was removed in gaseous form, and the polymer powder was dried at 80° C./100 mbar.

2.25 kg of polypropylene were obtained, corresponding to an activity of the metallocene mixture of 218.5 kg of PP/g of metallocene×h.

VN=91 cm³ /g; M_(w) =72,800 g/mol, M_(w) /M_(n) =4.6, II=96.8%.

EXAMPLE 14

Example 1 was repeated, but the metallocenes used were 5.4 mg (0.010 mmol) of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride and 27.0 mg (0.056 mmol) of rac-dimethylsilyl(2-methyl-4,5,6,7-tetrahydro-1-indenyl)₂ zirconium dichloride, the polymerization temperature was 50° C., and the polymerization time was 1.5 hours.

1.51 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 31.1 kg of PP/g of metallocene×h.

VN=187 cm³ /g; M_(w) =132,500 g/mol, M_(w) /M_(n) =4.1, II=97.6%.

EXAMPLE 15

Example 1 was repeated, but the metallocenes used were 4.8 mg (0.010 mmol) of rac-dimethylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 7.0 mg (0.017 mmol) of rac-ethylene(1-indenyl)₂ zirconium dichloride. The polymerization temperature was 50° C. and the polymerization duration was 1 hour.

1.50 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 127.1 kg of PP/g of metallocene×h.

VN=125 cm³ /g; M_(w) =129,500 g/mol, M_(w) /M_(n) =5.3, II=95.4%.

EXAMPLE 16

Example 1 was repeated, but the metallocenes used were 6.0 mg (0.010 mmol) of rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride, 6.0 mg (0.013 mmol) of rac-dimethylsilyl(1-indenyl)₂ zirconium dichloride and 36.0 mg (0.083 mmol) of rac-dimethylsilyl(2,3,5-trimethylcyclopentadienyl)₂ zirconium dichloride, the polymerization temperature was 40° C. and the polymerization duration was 2 hours.

1.79 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 18.6 kg of PP/g of metallocene×h.

VN=267 cm³ /g, M_(w) =293,000 g/mol, M_(w) /M_(n) =5.7, II=98.0%, MFI (230/5)=24.6 g/10 min.

EXAMPLE 17

A dry 24 dm³ reactor was flushed with propylene and filled with 12 dm³ of liquid propylene and with 20 ml of a toluene solution of trimethylaluminum (corresponding to 52 mmol of AlMe₃). The batch was stirred at 30° C. for 15 minutes.

In parallel, 3.0 mg (0.005mmol) of rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride, 2.0 mg (0.004 mmol) of rac-dimethylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 2.0 mg (0.004 mmol) of rac-dimethylgermyl(1-indenyl)₂ zirconium dichloride were dissolved in 20 cm³ of methylaluminoxane solution (27 mmol of Al, toluene), and, after 15 minutes, the solution was introduced into the reactor. The mixture was polymerized at 65° C. for 1.5 hours.

1.59 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 151.4 kg of PP/g of metallocene×h.

VN=153 cm³ /g; M_(w) =195,000 g/mol, M_(w) /M_(n) =5.8, II=96.0%, MFI (230/5)=87 g/10 min.

EXAMPLE 18

Example 1 was repeated, but the metallocenes used were 6.0 mg (0.01 mmol) of rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 45.0 mg (0.108mmol) of rac-methylene(3-t-butyl-1-cyclopentadienyl)₂ zirconium dichloride, the polymerization temperature was 40° C. and the polymerization duration was 4 hours.

1.63 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 8.0 kg of PP/g of metallocene×h.

VN=358 cm³ /g; M_(w) =354,000 g/mol, M_(w) /M_(n) =12.5, II=93.5%.

EXAMPLE 19

Example 1 was repeated, but the metallocenes used were 6.0 mg (0.010 mmol) of rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 6.0 mg (0.012 mmol) of rac-dimethylsilyl(4,7-dimethyl-1-indenyl)₂ zirconium dichloride, the polymerization temperature was 40° C. and the polymerization duration was 2 hours.

0.85 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 35.4 kg of PP/g of metallocene×h.

VN=324 cm³ /g; M_(w) =352,500 g/mol, M_(w) /M_(n) =15.5, II=95.3%.

EXAMPLE 20

Example 1 was repeated, but the metallocenes used were 6.0 mg (0.010 mmol) of rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride and 7.2 mg (0.016 mmol) of rac-ethylene(2-methyl-1-indenyl)₂ zirconium dichloride. The polymerization temperature was 50° C. and the polymerization duration was 2 hours.

1.44 kg of polypropylene were obtained, corresponding to an activity of the metallocene system of 54.6 kg of PP/g of metallocene×h.

VN=227 cm³ /g; M_(w) =406,000 g/mol, M_(w) /M_(n) =8.0, II=97.1%.

EXAMPLE 21

Example 20 was repeated, but in addition 75 g of ethylene were metered in continuously during the polymerization. The polymerization temperature was 60° C. and the polymerization time was 1 hour.

1.65 kg of ethylene-propylene copolymer were obtained, corresponding to an activity of the metallocene system of 125.0 kg of copolymer/g of metallocene×h.

VN=291 cm³ /g; M_(w) =387,000 g/mol, M_(w) /M_(n) =7.4; 4.2% ethylene content with ethylene units predominantly incorporated in an isolated manner (¹³ C-NMR analysis).

EXAMPLE 22

Example 21 was repeated, but 300 g of ethylene were only added after a polymerization time of 30 minutes.

1.49 kg of copolymer were obtained, corresponding to an activity of the metallocene system of 112.9 kg of copolymer/g of metallocene×h.

VN=357 cm³ g; M_(w) =449,000 g/mol, M_(w) /M_(n) =8.8. The polymer product can be separated by fractionation (decane, diethyl ether) into a polypropylene component and an ethylene-propylene rubber component.

Ethylene content of the copolymer 18.4%.

EXAMPLE 23

A dry 150 dm³ reactor was flushed with nitrogen and filled at 20° C. with 80 dm³ of a gasoline fraction with the aromatics removed and with a boiling range of 100°-120° C. The gas space was then flushed free from nitrogen by injecting 2 bar of propylene and releasing the pressure, and repeating this cycle four times.

50 l of liquid propylene were added, and 64 cm³ of a toluene solution of methylaluminoxane (corresponding to 100 mmol of Al, molecular weight 990 g/mol according to cryoscopic determination) were added and the reactor contents were heated to 50° C.

Hydrogen was metered in to give a hydrogen content in the gas space of the reactor of 0.1%, and this content was then maintained during the entire polymerization time by topping up (monitoring on-line by gas chromatography).

15.3 mg of rac-methylethylene(2-methyl-1-indenyl)₂ zirconium dichloride (0.033 mmol), 6.3 mg of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride (0.012 mmol) and 7.0 mg of rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride (0.012mmol) were dissolved in 32 ml of a toluene solution of methylaluminoxane (corresponding to 50 mmol of Al) and, after 15 minutes, the solution was introduced into the reactor.

The reactor was kept at a polymerization temperature of 50° C. for 7 hours by cooling, the polymerization was then terminated by addition of 2 bar of CO₂ gas, and the polymer formed was separated from the suspension medium in a pressure filter. The product was dried for 24 hours at 80° C./200 mbar. 16.4 kg of polymer powder, were obtained corresponding to a metallocene activity of 81.9 kg of PP/g of metallocene×h.

VN=206 cm³ /g; M_(w) =248,000 g/mol; M_(w) /M_(n) =3.4 II=97.9%; MFI (230/5)=32 g/10 min, m.p.: 151° C.

The product had the following mechanical data: Modulus of elasticity in tension (in accordance with DIN 53457-Z) 1,430 N/mm² ; notched impact strength (a_(n) in accordance with DIN 53453) 5 mJ/mm² at 23° C.; Izod impact strength (in accordance with ISO 180/1 C) 69 mJ/mm² at 23° C. and 12 mJ/mm² at -30° C.; Izod notched impact strength (according to ISO 180/1 A) 3 mJ/mm² at 23° C. and 2 mJ/mm² at -30 ° C.; ball indentation hardness (pressing, conditioned, 358N) 84N/mm² and ball indentation hardness (injection molding, 358N, in accordance with DIN 53456) 75N/mm².

EXAMPLE 24

Example 23 was repeated but the metallocene mixture comprised 6.3 mg of rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride (0.012 mmol) and 2.9 mg of rac-dimethylsilyl(1-indenyl)₂ zirconium dichloride (0.006 mmol). Polymerization was carried out without hydrogen.

The polymerization was complete after 20 hours. 18.7 kg of polymer powder were obtained, corresponding to a metallocene activity of 101.6 kg of PP/g of metallocene×h.

VN=202 cm³ /g; M_(w) =296,000 g/mol; M_(w) /M_(n) =7.9 II=96.4%; MFI (230/5)=39 g/10 min; m.p.: 148° C.

The product had the following mechanical data: Modulus of elasticity in tension (in accordance with DIN 5347-Z) 1,280N/mm² ; notched impact strength (a_(n) in accordance with DIN 53453) 3 mJ/mm² at 23° C.; Izod impact strength (in accordance with ISO 180/1 C) 65 mJ/mm² at 23° C. and 11 mJ/mm² at -30° C.; Izod notched impact strength (according to ISO 180/1 A) 3 mJ/mm² at 23° C. and 2 mJ/mm² at -30° C.; ball indentation hardness 77N/mm² (pressing, conditioned, 358N) and 71N/mm² (injection molding, 358N, in accordance with DIN 53 456). 

We claim:
 1. A catalyst comprising an aluminoxane and a transitional metal component comprising at least one zirconocene of the formula I and at least one zirconocene of the formula Ia or alternatively, at least two zirconocenes of the formula I ##STR12## in which R¹ and R² are identical or different and are a hydrogen atom, a C₁ -C₁₀ -alkyl group, a C₁ -C₁₀ -alkoxy group, a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -aryloxy group, a C₂ -C₁₀ -alkenyl group, a C₇ -C₄₀ -arylalkyl group, a C₇ -C₄₀ -alkylaryl group, a C₈ -C₄₀ -arylalkenyl group or a halogen atom,R³ and R⁴ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group which is halogenated, a C₆ -C₁₀ -aryl group, or a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or --PR₂ ¹⁰ radical, in which R¹⁰ is a halogen atom, a C₁ -C₁₀ -alkyl group or a C₆ -C₁₀ -aryl group, R⁵ and R⁶ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group which optionally are halogenated, a C₆ -C₁₀ -aryl group, or a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or --PR₂ ¹⁰ radical, in which R¹⁰ is a halogen atom, a C₁ -C₁₀ -alkyl group or a C₆ -C₁₀ -aryl group, with the proviso that both R⁵ and R⁶ are not hydrogen, R⁷ is ##STR13## ═BR¹¹, ═AlR¹¹, --Ge--, --Sn, --O--, --S--, ═SO, ═SO₂, ═NR¹¹, ═CO, ═PR¹¹ or ═P(O)R¹¹, R¹¹, R¹² and R¹³ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group, a C₁ -C₁₀ -fluoroalkyl group, a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -fluoroaryl group, a C₁ -C₁₀ -alkoxy group, a C₂ -C₁₀ -alkenyl group, a C₇ -C₄₀ -arylalkyl group, a C₈ -C₄₀ -arylalkenyl group or a C₇ -C₄₀ -alkylaryl group, or R¹¹ and R¹² or R¹¹ and R¹³, together with the atoms connecting them, in each case form a ring, and M¹ is silicon, germanium or tin, R⁸ and R⁹ are identical or different and are as defined for R¹¹, R¹⁴ and R¹⁵ are identical or different and are monocyclic or polycyclic hydrocarbon radicals which can form a sandwich structure together with the zirconium atom, and m and n are identical or different and are zero, 1 or 2, where m plus n is zero, 1 or
 2. 2. The catalyst as claimed in claim 1, wherein, in the formula I, R¹ and R² are identical or different and are methyl or chlorine, R³ and R⁴ are hydrogen, R⁵ and R⁶ are identical or different and are methyl, ethyl or trifluoromethyl, R⁷ is a ##STR14## radical, and n plus m is zero or
 1. 3. The catalyst as claimed in claim 1, wherein the compound of the formula I is rac-dimethylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride, rac-ethylene(2-methyl-1-indenyl)₂ zirconium dichloride, rac-diphenylsilyl(2-methyl-1-indenyl)₂ zirconium dichloride, rac-methylethylene(2-methyl-1-indenyl)₂ zirconium dichloride or rac-phenyl(methyl)silyl(2-methyl-1-indenyl)₂ zirconium dichloride.
 4. The process as claimed in claim 1, wherein, in the formula Ia, R¹ and R² are identical or different and are methyl or chlorine, ##STR15## radical, n+m is zero or 1 andR¹⁴ and R¹⁵ are identical or different and are fluorenyl, indenyl or substituted cyclopentadienyl.
 5. The catalyst as claimed in claim 1, wherein the compound of the formula Ia is rac-phenyl(methyl)silyl(indenyl)₂ zirconium dichloride, diphenylmethylene(9-fluorenyl)(cyclopentadienyl)zirconium dichloride, isopropylidene(9-fluorenyl)(cyclopentadienyl)zirconium dichloride, rac-dimethylsilyl(2,3,5-trimethyl-1-cyclopentadienyl)₂ zirconium dichloride, rac-dimethylsilyl(indenyl)₂ zirconium dichloride, rac-dimethylgermyl(indenyl)₂ zirconium dichloride, rac-dimethylsilyl(indenyl)₂ dimethylzirconium, rac-phenyl(vinyl)silyl(indenyl)₂ zirconium dichloride, ##STR16## rac-dimethylsilyl(2,4-dimethylcyclopentadienyl)₂ zirconium dichloride, rac-isopropylidene(indenyl)₂ zirconium dichloride, rac-dimethylsilyl(2-methyl-4,5,6,7-tetrahydro-1-indenyl)₂ zirconium dichloride, rac-ethylene(indenyl)₂ zirconium dichloride, rac-methylene(3-t-butyl-1-cyclopentadienyl)₂ zirconium dichloride or rac-dimethylsilyl(4,7-dimethyl-1-indenyl)₂ zirconium dichloride.
 6. The transitional metal component as claimed in claim 1, wherein R¹ and R² are identical or different and are a hydrogen atom, a C₁ -C₃ -alkyl group, a C₁ -C₃ -alkoxy group, a C₆ -C₈ -aryl group, a C₆ -C₈ -aryloxy group, a C₂ -C₄ -alkenyl group, a C₇ -C₁₂ -alkylaryl group, a C₈ -C₁₂ -arylalkenyl group or chlorine andR³ and R⁴ are identical or different and are a hydrogen atom, a fluorine atom, a chlorine atom, a bromine atom, a C₁ -C₄ -alkyl group which is halogenated, a C₆ -C₈ -aryl group, a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or PR₂ ¹⁰ radical in which R¹⁰ is a chlorine atom, a C₁ -C₃ -alkyl group or a C₆ -C₈ -aryl group, and wherein R⁵ and R⁶ are identical or different and are C₁ -C₄ -alkyl which is optionally halogenated and R¹¹, R¹² and R¹³ are identical or different and are methyl CF₃ group, C₆ -C₈ -aryl group, pentafluorophenyl group, C₁ -C₄ -alkoxy group, C₂ -C₄ -alkenyl group, C₇ -C₁₀ -arylalkyl group, C₈ -C₁₂ -arylalkenyl group or C₇ -C₁₂ -alkylaryl group and M¹ is silicon or germanium.
 7. The catalyst as claimed in claim 1, where R³ and R⁴ are identical or different and are a hydrogen atom, a C₆ -C₁₀ -aryl group, or a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or --PR₂ ¹⁰ radical, in which R¹⁰ is a halogen atom, a C₁ -C₁₀ -alkyl group or a C₆ -C₁₀ -aryl group.
 8. The catalyst as claimed in claim 1, wherein the aluminoxane is of the formula II ##STR17## for the linear type and/or of the formula III ##STR18## wherein for the formulae II and III, the radicals R may be identical or different and are a C₁ -C₆ -alkyl group, a C₁ -C₆ -fluoroalkyl group, a C₆ -C₁₈ -aryl group, a C₁ -C₆ -fluoroaryl group or hydrogen and n is an integer from 0 to
 50. 9. The catalyst as chimed in claim 8, which further comprises that the aluminumoxane of formula II and/or of formula III is mixed with the compound AlR³, wherein the radicals R may be identical or different and are a C₁ -C₆ -alkyl group, a C₁ -C₆ -fluoroalkyl group, a C₆ -C₁₈ -aryl group, a C₁ -C₆ -fluoroaryl group or a hydrogen.
 10. The catalyst as claimed in claim 8, wherein said aluminoxane is methylaluminoxane.
 11. A transitional metal component comprising at least one zirconocene of the formula I and at least one zirconocene of the formula Ia or alternatively, at least two zirconocenes of the formula I ##STR19## in which R¹ and R² are identical or different and are a hydrogen atom, a C₁ -C₁₀ -alkyl group, a C₁ -C₁₀ -alkoxy group, a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -aryloxy group, a C₂ -C₁₀ -alkenyl group, a C₇ -C₄₀ -arylalkyl group, a C₇ -C₄₀ -alkylaryl group, a C₈ -C₄₀ -arylalkenyl group or a halogen atom,R³ and R⁴ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group which is halogenated, a C₆ -C₁₀ -aryl group, or a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or --PR₂ ¹⁰ radical, in which R¹⁰ is a halogen atom, a C₁ -C₁₀ -alkyl group or a C₆ -C₁₀ -aryl group, R⁵ and R⁶ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group, which optionally are halogenated, a C₆ -C₁₀ -aryl group, or a --NR₂ ¹⁰, --SR¹⁰, --OSiR₃ ¹⁰, --SiR₃ ¹⁰ or --PR₂ ¹⁰ radical, in which R¹⁰ is a halogen atom, a C₁ -C₁₀ -alkyl group or a C₆ -C₁₀ -aryl group, with the proviso that both R⁵ and R⁶ are not hydrogen, R⁷ is ##STR20## ═BR¹¹, ═AlR¹¹, --Ge--, --Sn, --O--, --S--, ═SO, ═SO₂, ═NR¹¹, ═CO, ═PR¹¹ or ═P(O)R¹¹, R¹¹, R¹² and R¹³ are identical or different and are a hydrogen atom, a halogen atom, a C₁ -C₁₀ -alkyl group, a C₁ -C₁₀ -fluoroalkyl group, a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -fluoroaryl group, a C₁ -C₁₀ -alkoxy group, a C₂ -C₁₀ -alkenyl group, a C₇ -C₄₀ -arylalkyl group, a C₈ -C₄₀ -arylalkenyl group or a C₇ -C₄₀ -alkylaryl group, or R¹¹ and R¹² or R¹¹ and R¹³, together with the atoms connecting them, in each case form a ring, and M¹ is silicon, germanium or tin, R⁸ and R⁹ are identical or different and are as defined for R¹¹, R¹⁴ and R¹⁵ are identical or different and are monocyclic or polycyclic hydrocarbon radicals which can form a sandwich structure together with the zirconium atom, and m and n are identical or different and are zero, 1 or 2, where m plus n is zero, 1 or
 2. 12. The transitional metal component as claimed in claim 9, wherein, in the formula I, R¹ and R² are identical or different and are methyl or chlorine, R³ and R⁴ are hydrogen, R⁵ and R⁶ are identical or different and are methyl, ethyl or trifluoromethyl, R⁷ is a ##STR21## and n plus m is zero or
 1. 13. The transitional metal component as claimed in claim 11, wherein R¹⁴ and R¹⁵ are identical or different and are indenyl ligands which carry substitutents which are a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -fluoroaryl group, a C₇ -C₄₀ -arylalkyl group, a C₈ -C₄₀ -arylalkenyl group, a C₇ -C₄₀ -alkylaryl group or two substituents together with the atoms connecting them form a ring.
 14. The transitional metal component as claimed in claim 13, wherein the indenyl ligands carry a C₆ -C₁₀ -aryl group, a C₆ -C₁₀ -fluoroaryl group, a C₇ -C₄₀ -arylalkyl group, a C₈ -C₄₀ -arylalkenyl group, a C₇ -C₄₀ -alkylaryl group or two substituents together with the atoms connecting them form a ring.
 15. The transitional metal component as claimed in claim 14, wherein the indenyl ligands carry a C₆ -C₁₀ -aryl group or two substituents together with the atoms connecting them form a ring. 